We thank Prof. H.-T. Chu for the BET measurements and
Prof. Ikai Wang (NTHU) for the TPR experiments. The
Institute of Nuclear Energy Research (contract NL940251),
MOE ATU program, and National Science Council (contracts
NSC 94-2120-M-009-014, 98-2113-M-009-007-MY3) supported
this research. MCL acknowledges the Taiwan Semi-
conductor Manufacturing Co. for the TSMC Distinguished
Professorship and the Taiwan National Science Council for
the Distinguished Visiting Professorship at the National Chiao
Tung University.
Fig. 4 (a) Hydrogen selectivity over catalysts with Ce1ꢀx
samples with different morphologies. (b) Hydrogen consumption rate
observed from TPR profiles over Ce1ꢀx samples.
x 2
M O
x 2
M O
The catalytic activity was evaluated in terms of hydrogen
selectivity (SH2), which is defined as the molar ratio of the
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6
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3
288 | Chem. Commun., 2010, 46, 3286–3288
This journal is ꢁc The Royal Society of Chemistry 2010